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CN103861490B - Static mixer - Google Patents

Static mixer Download PDF

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Publication number
CN103861490B
CN103861490B CN201310742011.2A CN201310742011A CN103861490B CN 103861490 B CN103861490 B CN 103861490B CN 201310742011 A CN201310742011 A CN 201310742011A CN 103861490 B CN103861490 B CN 103861490B
Authority
CN
China
Prior art keywords
static mixer
mounting body
wall segment
longitudinal axis
cross
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201310742011.2A
Other languages
Chinese (zh)
Other versions
CN103861490A (en
Inventor
S.哈比比-奈尼
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Medmis Switzerland Ag
Original Assignee
Sulzer Mixpac AG
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sulzer Mixpac AG filed Critical Sulzer Mixpac AG
Publication of CN103861490A publication Critical patent/CN103861490A/en
Application granted granted Critical
Publication of CN103861490B publication Critical patent/CN103861490B/en
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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/431—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor
    • B01F25/4314—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor with helical baffles
    • B01F25/43141—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor with helical baffles composed of consecutive sections of helical formed elements
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/432—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction with means for dividing the material flow into separate sub-flows and for repositioning and recombining these sub-flows; Cross-mixing, e.g. conducting the outer layer of the material nearer to the axis of the tube or vice-versa
    • B01F25/4321—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction with means for dividing the material flow into separate sub-flows and for repositioning and recombining these sub-flows; Cross-mixing, e.g. conducting the outer layer of the material nearer to the axis of the tube or vice-versa the subflows consisting of at least two flat layers which are recombined, e.g. using means having restriction or expansion zones
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
    • B29C44/02—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles for articles of definite length, i.e. discrete articles
    • B29C44/12—Incorporating or moulding on preformed parts, e.g. inserts or reinforcements
    • B29C44/14—Incorporating or moulding on preformed parts, e.g. inserts or reinforcements the preformed part being a lining
    • B29C44/16—Incorporating or moulding on preformed parts, e.g. inserts or reinforcements the preformed part being a lining shaped by the expansion of the material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
    • B29C44/34—Auxiliary operations
    • B29C44/36—Feeding the material to be shaped
    • B29C44/38—Feeding the material to be shaped into a closed space, i.e. to make articles of definite length
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
    • B29C44/34—Auxiliary operations
    • B29C44/36—Feeding the material to be shaped
    • B29C44/38—Feeding the material to be shaped into a closed space, i.e. to make articles of definite length
    • B29C44/42—Feeding the material to be shaped into a closed space, i.e. to make articles of definite length using pressure difference, e.g. by injection or by vacuum
    • B29C44/428—Mould constructions; Mould supporting equipment
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor

Landscapes

  • Chemical & Material Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Mechanical Engineering (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Injection Moulding Of Plastics Or The Like (AREA)
  • Molding Of Porous Articles (AREA)
  • Moulds For Moulding Plastics Or The Like (AREA)

Abstract

The invention provides a method for manufacturing a static mixer in an injection process. The method comprises the following steps: a polymer melt containing a foaming agent is injected through the injection point and into the passage at an injection pressure of less than 500 bar. The passage is filled with the polymer melt and the polymer melt is allowed to at least partially foam in the passage. The ratio of the length of flow path to the height of flow path is >= 10. The static mixer comprises an installation body for installation into a tubular mixer housing of a static mixer. An injection molding tool is used for manufacturing a static mixer. The installation body is provided with a longitudinal dimension and a diameter. The ratio of longitudinal dimension to the diameter is >= 1. The installation body is at least partially made of foamed plastic. The ratio of the longitudinal dimension to the wall thickness is >= 10, and the ratio of length of the flow path to the wall thickness is >= 10.

Description

Static mixer
The application is the original bill applying date on October 19th, 2009, Application No. 200910179797.5, entitled 《Static mixer》Application for a patent for invention divisional application.
Technical field
The present invention relates to a kind of plastic static mixer, the static mixer is included for installed in blender tubulose Mounting body in housing.The mounting body has longitudinal axis, and the longitudinal axis flow into the direction row of mounting body along fluid Row, so that the mounting body can cross over blending space.The blending space has horizontal stroke in the plane of longitudinal axis The flow area for cuing open（Or region）, the cross-sectional flow area corresponds essentially to the cross-sectional flow surface of blender tubular shell Product.The mounting body includes wall segment, and for separating and/or making the fluid stream by fluid stream, to deflect into deviation described vertical On the direction of axis.The invention further relates to a kind of method for manufacturing this static mixer.
Background technology
For example from this static mixer known to patent document EP1426099B1.In this static mixer, by three Two kinds of compositions or component is made to be mixed with each other by multiple hydrid components of same type in the mixed process of part composition, it is mixed at this During conjunction, first material is separated, material is spread and is shifted.Depending on it is each into physical property, it is this to mix Cheng Bixu implements multiple.For this purpose, the mounting body or apparatus main body of multiple same configurations are sequentially disposed at the static mixing In device, these blenders are particularly used for a small amount of composition, i.e., several milliliters to about 1000 milliliters, mixing.Thus, these mix The blending space of clutch has the diameter and the length more than 50mm less than 10mm.This has following results, the i.e. blender The wall thickness of wall segment is likely to be breached less than 1mm, frequently even less than 0.5mm.
Preferably manufactured with injection moulding process according to the plastic blender of patent document EP1426099B1.Using injection Process manufacture before the blender less than the 30mm length of 3mm wall thickness be it is impossible because from the decanting point of injection moulding tool to The flow path of the end being oppositely arranged of blender needs very high in-house tool pressure.So will be ensured that, farthest Wall segment from the blender of decanting point is also completely filled with polymer melt, it is necessary to provide the in-house tool pressure more than 1000 bars Power.When the static mixer of thin-walled must be manufactured with above-mentioned size, before traditional injection moulding tool, can not undergo these High in-house tool pressure.Thus, so far in injection moulding process, economically fabricate wall thickness and be less than 3mm and mixer length and wall Blender of the ratio of thickness more than 10, particularly plastic blender, is impossible.Blender is being manufactured by injection moulding process During known quiescent state blender of the ratio of length and wall thickness more than 10, it is necessary to which the formation of shrink mark is regarded as further problem.Even It is in the case of the in-house tool pressure more than 1000 bars, several in can not preventing with such as patent document EP1426099B1 The static mixer of what shape has shrink mark.
The content of the invention
It is an object of the invention to provide a kind of improvement to existing static mixer and existing method, so that energy By static mixer of the injection moulding process manufacture with relatively thin wall thickness and greater depth.
The purpose of the present invention is able to reality by a kind of method for by noting system or injection moulding process manufacture static mixer Existing, the method comprising the steps of：Will be comprising foaming agent with the injection pressure less than 500 bars in decanting point or injection position Polymer melt injection channel in；Fill the passage with the polymer melt comprising foaming agent, it is described comprising foaming agent Polymer melt at least partly bubbles in the passage, and wherein flow path reaches at least 10 with the ratio of wall thickness.
Relative to traditional injection molding process, the polymer comprising foaming agent is used for the manufacture of static mixer, and which is in injection During or directly bubble after injection it.
Note method of the invention is especially included with less than 300 bars, particularly preferably less than 200 bars, injection Polymer comprising foaming agent is injected into the step in note instrument by pressure.
Methods described then comprises the following steps until removing from static mixer：Be cooled in the passage comprising send out The polymer melt of at least part of foaming of infusion；The polymer melt is made to solidify to form static mixer；Expand described The section of passage；Remove the static mixer.
The injection of the polymer comprising foaming agent advantageously starts from single decanting point or position.
Polymer comprising foaming agent bubbles at least in farthest away from the region of the decanting point.Reduced by foam plasticss Amount of polymer needed for the blender of each manufacture, because the foam plasticss include bubble.These bubbles it is average straight Footpath is advantageously not more than 100 μm, preferably not more than 50 μm, particularly preferably no more than 10 μm.
A kind of note tool kit that the mounting body for static mixer is manufactured with the polymer melt comprising foaming agent Include passage and for the polymer melt comprising foaming agent is introduced into the inlet in the passage, passage substantially has to be used for There is ratio to be at least 10 flow path and the ratio of wall thickness for each size of the mounting body of static mixer and passage.Flowing road Footpath can especially be more than 50, preferably more than 140 with the ratio of wall thickness, particularly preferably more than 180.In the region of inlet Injection pressure is less than 500 bars.Injection pressure is preferably less than 300 bars, particularly preferably less than 200 bars.
The passage of note instrument has a longitudinal axis, the longitudinal axis it is substantially corresponding with the longitudinal axis of the part and With cross-section channel area（Or cross-sectional passage area）, the cross-section channel area is arranged substantially perpendicular to described The flow direction of polymer melt, the cross-section channel area have width dimensions and thickness.Thickness is substantially Corresponding to the wall thickness of static mixer, and passage has the geometry of static mixer.
Thickness reaches no more than 2.5mm, preferably not more than 2.3mm, particularly preferably no more than 2mm.
Depending on the geometry of static mixer, the passage can have main channel and multiple wing passages.
First wing passage has a shape of plate-like piece, and the plate-like piece is by the length of the wing passage, width dimensions and thickness Degree size determines.Prolong in direction of the length of the plate-like piece of first wing passage substantially along the longitudinal axis of the passage Stretch, be arranged to by the cross-section channel area of width dimensions and thickness leap and be substantially perpendicular to length.
Second wing passage of the shape with plate-like piece can be set, and its thickness direction substantially longitudinally extends And the horizontal layout crossed over by longitudinal size and width dimensions is into angled relative to longitudinal axis.The plane is especially Can be arranged with 90 ° of angles.
Plate-like piece can include that certain curvature or bending, i.e. one of longitudinal size and width dimensions include Curved Shape.
According to the preferred embodiment for noting instrument processed, mixing nozzle can be arranged in the upstream of the import for reaching passage, in order to Polymer melt comprising foaming agent homogenizes.
The purpose of the present invention is accomplished by a kind of static mixer, and the static mixer is included for installing Mounting body in blender tubular shell, the mounting body have longitudinal direction and radial dimension or diameter, for non- For circular blender tubular shell, the diameter is corresponding to when the cross-sectional area of blender tubular shell is square The length of side, for the mixer case of other shapes, such as the mixer case with rectangle or oval cross section is equivalent Diameter DaIt is determined under following assumed condition：If cross-sectional area is circular, i.e., using formula Da=2*（A/Π）。 Wherein DaRepresent equivalent diameter；A represents the cross-sectional area of reality.Longitudinal size is at least 1 with diameter ratio, it is necessary to circular horizontal stroke The equivalent diameter of the diameter or non-circular cross sections in section is used as diameter.Mounting body is made up of foam plasticss at least in part. Provided that single mounting body, then longitudinal direction side of the longitudinal size corresponding to mounting body.If multiple mounting bodies each other before After arrange, then longitudinal size derives from longitudinal direction side sum.Longitudinal size can especially be more than 3 with diameter ratio, preferably more than 5, particularly preferably more than 7.Due at a fairly low in-house tool pressure, so the static mixer of the length of macrotectonics is especially Can be economically fabricated.Relatively low in-house tool pressure is caused due to following truth：Plastics used are with comprising foaming agent Polymer form occur, the polymer bubbles during injection molding process, so that being made up of foam plasticss at least in part Mounting body occur in after injection molding process terminates.For this mounting body as static mixer, road of flowing Footpath is at least 10 with the ratio of wall thickness.Flow path especially can be especially excellent more than 50, preferably more than 140 with the ratio of wall thickness Selection of land is more than 180.
As the foaming agent that can be rendered as physically or chemically foaming agent reduces the viscosity of polymer, so including foaming agent Polymer with the lower viscosity of the similar polymer than no foaming agent.Especially can be molten using such a polymer Body, the polymer melt include physical gas, particularly supercritical gas such as CO2, or CBA, and which is rendered as Single phase soln.Foam plasticss have micropore or microcavity, and the micropore can be provided with the pore size less than 100 μm, at least above About 106Micropore/cm3Pore density.In order to manufacture static mixer with foam plasticss, under stress by flowable material It is incorporated into note instrument.The note instrument defines the cavity of the shape with static mixer.For the polymerization in foaming The solution of supercritical fluid is obtained in thing, specific incorporation time is needed, the wall of static mixer is thinner, and the incorporation time is got over It is few.
In order to manufacture static mixer, in the first process steps, plastic pellet is made to melt in extruder.It is subsequently adding and sends out Infusion, such as foaming agent of the addition in supercritical gas form, particularly CO2.On the one hand, can be by activating suitable through-flow tune Section valve adds foaming agent in the select location of plastification screw bolt.The temperature and pressure of foaming agent is adjusted so that foaming agent changes to which Supercriticality.Also foaming agent can be preheated before foaming agent is introduced, to avoid the unexpected pressure in higher temperature from increasing.As Its alternative, can add foaming agent, outside plasticizing chamber especially as supercritical fluid.Subsequently make to send out by plastification screw bolt Infusion in plasticizing chamber with Mixing of Polymer Melt.It is straight then to the diffusion in polymer that this mixed process increases foaming agent To foaming agent saturation in the polymer.The contact area of bi-material is expanded by mixed process, thus for diffusion process The required depth of penetration reduces.Therefore, the polymer mixed of foaming agent and fusing is made by the motion of plastification screw bolt, this contributes to The solution of foaming agent is produced in the polymer.As long as plastification screw bolt rotates, it is just in foaming agent/polymer system to be mixed Produce the shearing field of two dimension.In this respect, stretched on shear direction by the bubble that foaming agent is formed, the disturbance of laminar flow makes to be drawn The bubble stretched resolves into less spherical bubbles.Plastification screw bolt advantageously has the blade of irregular arrangement, so that foaming agent/ The orientation of the separating surface of polymer changes in the relation of streamline, and the efficiency for taking this stratiform mixing is improved.It is quiet using In the mixed process of state blender, the diffusion of bubble also occurs in the polymer melt for surrounding each bubble.Biphasic mixture Subsequently occur only in diffuser casing to the conversion of single phase soln.In single phase soln, the concentration of foaming agent is substantially consistent , so solution can be considered as homogenizing.
After diffusion, quick heated solution takes this nucleation in saturated solution.Nucleation is understood to A kind of karyogenesis, which represents the basis of formation of the foam of the mean pore size with 100 μm of maximum.Due in polymer Foaming agent this higher temperature dissolubility reduce, so heating generate thermodynamic (al) unstability.When temperature increases When high, dissolubility reduces more, and nucleation rate is bigger, and the quantity of the micropore of nucleation is more.Maintain high pressure so that these Micropore will not have been generated in plasticizing chamber, and then the solution of the micropore with nucleation be incorporated into the hollow mould of note instrument In space processed.For example by being introduced into compressed air control pressure in instrument processed is noted.It is quick due to working as the pressure in note instrument Pressure instability during decline is qualitative, so micropore occurs in instrument processed is noted only grow, thus using poly- comprising foaming agent Flow resistance during compound reduces.Therefore, in-house tool pressure is reduced so that the pressure load of instrument is in ability in the range of permission Become possibility, the premature failure of instrument in allowed limits, can not promoted again.However, due to a variety of causes, it is pre- so far See with comprising this length of polymers manufacturing of foaming agent, the static mixer of thin-walled.On the one hand, it is basic it is not expected that energy This thin-walled blender with complex geometric shapes is produced by the reduction of injection rate, wherein the reduction of injection rate by Cause in the reduction of in-house tool pressure.It is referred to as condensing or solidifies in this phenomenon sector coil learnt from injection molding process. In this process, the solidification or solidification of the polymer melt being injected in note instrument occurs in the note system near corresponding wall In the region of instrument, this solidification can be caused by the thermograde between melt and wall, but this solidification it can also happen that In the instrument of the temperature with polymer melt, because the flow velocity of polymer melt is noting the close wall ratio of instrument processed near middle The region in region is low.It is corresponding with by the flowing of closed channel by the flowing for noting the polymer melt of instrument processed, it is this The flow molded line of the speed of flowing is substantially parabolical.The parabolical axis of symmetry is substantially indulged with the center of passage Axis is corresponding.Flow velocity has value 0 at the wall for noting instrument processed.Due to this flow molded line（Or flow diagram）, polymer There is in the passage formed by instrument processed is noted the different dwell times.Therefore, the larger dwell time of polymer melt make Into the low wall region of flow velocity, which has following results：Reaction, such as cross-linking reaction, or even also can in the case of without cooling down Occur inside polymer melt.Therefore there is the solidification of polymer melt in wall region.This has following results：Reduce still Can be used for the through-flow channel cross-section of polymer melt.In the case where corresponding part has 3mm with wall thickness, passage is horizontal This reduction in section is almost inessential, this is because solidification is confined to the zonule of the close wall of passage, so polymer is molten Physical ability flows through note instrument to manufacture the part of the wall thickness with more than 3mm in the case where there is no obstruction.
Each cross-sectional area has certain wall thickness, and longitudinal size reaches at least 40 with the ratio of wall thickness, preferably at least 50, particularly preferably at least 75.Cross-sectional area can be intersected with multiple wall segments, so wall thickness need not be by the instruction of cross-sectional area Individually it is determined clearly.However, the wall thickness of reality is conclusive for the design for noting instrument processed.This wall thickness is thinner, poly- It is more notable that polymer melt is injected into aforesaid wall effect during note instrument.It follows that the high in-house tool pressure of comparison Little wall thickness will be provided to.In the case of less than the in-house tool pressure for allowing, the wall thickness of static mixer may be little In 3mm, preferably less than 2mm, particularly preferably less than 1.5mm.
Especially multiple mounting bodies can be arranged each other in front and back along longitudinal axis.These mounting bodies can have identical Construction or heteroid mounting body can be combined each other, so as to produce a kind of mixer apparatus, such as patent document Shown in EP1312409B1.Adjacent mounting body is advantageously connected with each other, so as to be made up of the plurality of mounting body Blender make a monoblock type parts or part.This means that its entirety of blender is made in single note instrument Make.
The longitudinal size of mounting body or all mounting bodies can be between 5 to 500mm, preferably in 5 to 300mm Between, preferentially between 50 to 100mm.
Static mixer is advantageously so designed that so that mounting body has a longitudinal axis, and the longitudinal axis are along fluid stream Enter the direction orientation of the mounting body, so that the mounting body can be crossed over or across blending space, wherein the mixing Space has cross-sectional flow area in the plane of longitudinal axis（Or excessively stream region）, the cross-sectional flow area base In sheet corresponding to blender tubular shell cross-sectional flow area.The mounting body includes wall segment, for by fluid Stream separates and/or makes the fluid stream and deflects on the direction for deviateing longitudinal axis, can pass through the phase of wall segment and the plane Hand over and produce cross-sectional area, and the maximum of the cross-sectional area reaches the 1/5 of the cross-sectional flow area of blending space, preferably Ground reaches 1/10, particularly preferably reach 1/20.Mounting body is made up of foam plasticss at least in part, is using foam plasticss When, it has therefore been surprisingly found that identical flow path can be realized with much lower in-house tool pressure.Therefore, with prior art Compare, foam plasticss are used so that extending flow path becomes possibility, so the mixing with bigger longitudinal size can be manufactured Device.
First width is formed to side according to the cross-sectional area of the wall segment of first embodiment, be able to will be mixed to side by the first width Close space and be divided into two subregions, flow so as to mixed product stream, fluid stream passes are divided into two parts, it is empty depending on mixing Between in position from width to side, described two part streams can have same size or different size.Two can naturally also be formed Width above is flowed to side so as to correspondingly there is plural part.Due to the geometry of the complexity of static mixer, lead The polymer melt comprising foaming agent is caused by the frequent change of the note tool cross sections processed for flowing through.These changes are static mixed by being formed The geometry and arrangement of the wall segment of the mounting body of clutch is caused, relative to wall segment, it is necessary to noting instrument processed It is middle that corresponding cavity and passage are set.In this in particular cases carries out note instrument, pressure is adjusted, so that injecting In-house tool pressure is provided when journey starts, the polymer melt comprising foaming agent is still rendered as single-phase in the in-house tool pressure Solution, and this pressure is reduced during hollow molding space of the filling for the note instrument of static mixer.Pressure Power reduces causing foam is formed in injection process, particularly forms micro-pore diameter less than 100 μm and/or pore density More than at least about 106Micropore/cm3Foam.As foam has been formed during injection, so polymer melt Viscosity is reduced, this is because the micropore for occurring is produced as the bubble comprising compressible gases in two-phase state.Thus, this The viscosity that planting reduces is made it possible to relative to the traditional injection molding process for non-foaming composition under much lower in-house tool pressure Reduce injection rate.Due to relatively low viscosity, the particularly change in wall effect, the wall in the region of polymer melt deflection The change of effect, also occurs in that.
It is known for the simple geometric shape with substantial rectangular cross section, near implantation tool wall region It is less or at all non-foaming.If static mixer is especially by as described in one of geometry of more accurate description below Mounting body constitute, then the big deflection of fluid stream produced or result in each edge of wall segment and behind leading to Wall segment transition part office polymer melt flow path so that note work processed is arranged in the first wall segment Polymer melt in the marginal area in the aperture of tool is flowed in second wall region in the second following wall segment Heart district domain, and there is the shaping of two-phase foam.Thus, when injecting pressure and being as described above and reduce, due to adjacent wall-like Part arrangement angled each other, the arranged crosswise of particularly adjacent wall segment, foam forming is along blender Whole longitudinal size occurs.
The shape and the second width of substantial rectangular are had to side according to the wall segment of second embodiment, second width to While with the first width to while be oppositely disposed and according to preferred embodiment, described second it is wide to while relative to the first width to while rotate Certain angle, so as to form helical structure.
According to the 3rd advantageous embodiment, wall segment includes bars, and the first width of the bars is formed to side and divided Stream edge, the second width of the bars is adjacent with deflection piece to side, and the deflection piece is for by first from blending space The fluid stream of subregion is deflected in the Part II region of blending space.Wide made to side and the second width to border from first Wall segment surface direction arrangement substantially longitudinally and the surface of the deflection piece be arranged substantially at laterally In plane, the transverse plane is especially arranged relative at 45 ° to 90 ° angles of longitudinal axis, preferably into 60 ° to 90 ° angles, especially Preferably into 75 ° to 90 ° angles.
According to the with little dead band and the blender of the pressure drop for reducing and high mixed performance the 4th, particularly preferred reality Example is applied, mounting body includes multiple wall segments, and each wall segment has the cross section of substantial rectangular, substantial rectangular Cross section include first it is wide to while, the second width to while and first longitudinal direction side and second longitudinal direction side.
Wall segment is arranged in mounting body so that longitudinal side direction substantially longitudinally extends and institute State first it is wide to while and second width to while relatively described longitudinal axis direction extend transversely with.Mounting body includes the first wall Blending space is divided into two parts by shape part, first wall segment.At least two intersected with first wall segment Individual wall segment adjoins the first wall segment, and first wall segment is advantageous by least one transition piece and the second wall-like Part and the 3rd wall segment are connected.
Deflect mixed product stream by transition piece so that each composition or group into static mixer exists with being divided into stream stock Continuously separated during the path that they become the band that multiple width reduce through the static mixer, taken this also use This static mixer processes and is difficult to mix or the various composition with high viscosity.
Adjacent mounting body is connected with each other advantageous by least one connector.The construction of static mixer is due to institute State connector and become more rigid, so blender less easily occurs and blender energy relative to the bending of its longitudinal axis It is fitted in the pipe for surrounding blending space.
Can combine each other as required or combine according to the mounting body of previous embodiment.
Once corresponding note instrument is manufactured, due to above-mentioned static mixer manufacture and material cost just It is low, so above-mentioned static mixer can be suitable as disposable blender.Additionally, making in metering and/or mixing apparatus Use static mixer.Especially, multicomponent will can be contained（Or component）Cylinder（cartridge）It is considered as an example, the example Including discharger and the pipe for being connected to the discharger, and the static mixer containing one of with good grounds previous embodiment.
The static mixer can be installed to deliverying unit or discharge cylinder, be connected especially to containing on multicomponent cylinder. The static mixer can be used to for each flowable composition to be mixed into hardening mix products.Static mixer it is further Possible purposes is the mixing of the casting compound in gear division field or the mixing of multicomponent binding agent.
Description of the drawings
Below in conjunction with the description of the drawings present invention, wherein：
Fig. 1 is the first embodiment of blender of the invention；
Fig. 2 is the second embodiment of blender of the invention；
Fig. 3 is the 3rd embodiment of blender of the invention；And
Fig. 4 is the fourth embodiment of blender of the invention.
Specific embodiment
Figure 1 illustrates the first embodiment of static mixer of the invention.The static mixer includes peace The mounting body being mounted in unshowned tubular shell or apparatus main body 1, the tubular shell are risen positioned at the tubular shell The effect on the border of internal blending space 20.Generally by least two heterogeneities（Or component）The fluid to be mixed for constituting Flow through the blending space 20.In most of the cases, the composition or these compositions are using fluid state or as stickum Exist, this for example includes pastel, binding agent, but is also included within the fluid comprising medicament used in medical department or for changing The fluid of adornment purposes and food.This static mixer is also specifically used as disposable blender, for flowable composition Hardening mix products mixing, such as multicomponent（Or component）The mixing of binding agent.Another kind of preferred purposes is led in gear division The mixing of casting compound in domain.
Mounting body 1 does not have moving parts in itself（Or movable part）, so flowing of the mixed process by fluid itself To realize.Lack portable installed part（Or telecontrol equipment）This blender is counted as the master of the design of static mixer Want reason.The mounting body 1 has longitudinal axis 10, and the longitudinal axis 10 are also the longitudinal axis of tubular shell simultaneously.Longitudinal axis 10 are arranged along the main flow direction of fluid, that is, be in along being present in no any installed part（Or device）Or the tubulose of manifold On the direction of the flowing in housing.Additionally, the mounting body has diameter or radial dimension 36.If any desired At point, applying plane 21,121 perpendicular to this longitudinal axis is passed to blending space 20,120, then the cross-sectional stream for producing Dynamic area（Or excessively stream region）22nd, the 122 cross-sectional flow area one substantially with the blender tubular shell for being fitted without part Cause.Have to be noted that mounting body 1 is intersected with plane 21,121 in this respect, take this to produce cross-sectional area（Or cross section） Or cross-sectional region 23,123.
Thus, cross-sectional flow area 22,122 is less than mixer tube in the value in the region of wall segment or wall elements The value of the cross-sectional flow area of shape housing.Cross-sectional area（Or cross section）Maximum reach cross-sectional flow area 22,122 1/5.They are designed with wall as thin as possible as possible in the design of wall segment, so as to reduce as much as possible being used for The materials demand of the polymer of manufacture mounting body.It is such as viscous through the fluid of blender transmission under high pressure for having to For property fluid or pastel, 1/5 ratio of cross-sectional area of cross-sectional flow area is required.In this case, A certain degree of mechanical stability of blender is required.For the blender of the relatively low fluid of viscosity or shorter, can So that the ratio is reduced to 1/10 or less or or even 1/20 or less is reduced to.
For the mounting body 1 with least one plane of symmetry that blending space is substantially divided into two moieties Say, longitudinal axis are arranged approximately along this plane of symmetry.Mounting body 1 includes at least one wall segment 2,3,4,8,9, these wall-like Part for by fluid stream separate and/or make the fluid stream deflect into the direction for deviateing the longitudinal axis.Generally, fluid exists The both sides flowing of the wall segment.
Wall segment 2 is wide to side or first side 5 with first, described first it is wide to side 5 substantially in blending space Entirely extend on whole width or diametrically, that is, usually extend to the wall of tubular shell.Wall segment 2 is wide with being arranged in first To while 5 downstreams second it is wide to while or second side 6.According to Fig. 1, the second wall segment 8 adjoin described second it is wide to side 6 and after Followed by the 3rd wall segment 3, the 4th wall segment 9 is arranged in the downstream of the 3rd wall segment 3 and and with face Five wall segments 4 are adjacent.Wall segment 2 relative to longitudinal axis 10 have inclination angle, so as to two parts fluid stream it is inclined Turn by first it is wide to side 5 being formed.
According to the better simply modification not being shown specifically in figure, the wall segment 102 of adjacent mounting body 101 can be adjoined First wall segment 2（Or adjacent mounting body 101 adjoins mounting body 1）, the adjacent preferably cloth of mounting body 1,101 It is set to, especially 90 ° pivotably movable with respect each other of angle.Thus, mounting body 1 according to Fig. 1, 101 include a series of wall segment 2,3,4,102,103,104 and middleware 8,9,108,109, the wall segment 2,3, 4th, 102,103,104 arranged by alternately order relative to longitudinal axis 10 at an angle, and the interlude 8,9,108, 109 are arranged essentially parallel to longitudinal axis arrangement.Mounting body 101 also can rotate 180 ° relative to mounting body 1.
Figure 2 illustrates the mounting body or apparatus main body 1 of the static mixer of second embodiment.The mounting body In for installation into tubular shell, in such a case, it is possible to selectively tubular shell is manufactured into rectangle or rhombus Cross-sectional flow area can also be manufactured into the cross-sectional flow area with circular or ellipse.This mounting body 1 includes single wall segment 2, and the wall segment 2 is made with square surface or/and cross-sectional area（Or rectangular cross-sectional Face）23 plate shape part, the cross-sectional area 23 are corresponding with wall thickness 7.The cross-sectional area 23 is obtained using plane 21 Cross-sectional area or cross section as plate shape part, the plane 21 is vertically arranged relative to longitudinal axis 10, the longitudinal axis 10 axis of symmetry in main flow direction corresponding to the plate shape part.
In the case where the installed part such as mounting body of flowing deflection is not made, flowing and quilt of the fluid through blending space It is defined as main flow direction.Plate shape part with first it is wide to while 5 and second it is wide to while 6 and connect it is described two width to side Two longitudinal sides 25,35, first it is wide to while and second it is wide to while the blending space 20 crossed over by wall segment 2 is divided into into two The blending space is divided into two half-unit by individual part in the case of figure 2.In order to be able to make fluid along the stream of wall segment 2 Dynamic deflection, first it is wide to while 5 relative to second it is wide to while 6 reverse around longitudinal axis 10 so that two longitudinal sides 25,35 each idiomorphisms Into helix or the surface of helical structure.In the wall segment shown in Fig. 2, first it is wide to while 5 relative to second it is wide to while 6 quilts 180 ° of rotation.The longitudinal side 25,35 is preferably in contact with their tubular shell of encirclement or is arranged to from tubular shell at most Have one closely-spaced, so as to avoid the segment fluid flow stream of fluid from flowing in the clear and be excluded along the inwall of tubular shell Outside mixed process.
At least one other mounting body 101 can adjoin mounting body 1 successively；Illustrate only its cross-sectional area or Cross section 123.Cross-sectional area 123 first it is wide to while 105 be arranged to relative to mounting body 1 second it is wide to while into one jiao Degree.In the expression of Fig. 2, measure on cross-sectional flow area 122, relative angle reaches 900。
Fig. 3 illustrates another embodiment of static mixer, and the static mixer is included for installed in tubular shell In multiple mounting bodies or apparatus main body 1,101,201,301,401,501.First mounting body 1 is by with rectangular cross section Plate shape wall segment 2 constitute, the wall segment 2 include first it is wide to while 5, second it is wide to while 6, first longitudinal direction side 25 with And second longitudinal direction side 35.First it is wide be arranged in plane 21 to side 5, the plane 21 represents cross-sectional flow area 22, horizontal The flow area 22 for cuing open is arranged perpendicular to the main flow direction with reference to Fig. 1 definition.Two longitudinal sides 25,35 are in such case Under also contact unshowned tubular shell, or at most have little interval from tubular shell.
Wall segment 2 has the function of bars 26, and fluid stream is divided into two parts by the bars 26, except the Outside the deflection of the one wide edge to side 5, the deflection of the two parts is negligible.For this purpose, deflection piece 27 is in strip The adjacent bars 26 in the downstream of part.Deflection piece 27 is preferably provided in the plane parallel to the arrangement of plane 21 or relative to described Plane arranges that with certain inclination angle the inclination angle reaches no more than 60 °, preferably not more than 45 °, particularly preferably less In 30 °.Inclination angle between the surface of the deflection piece 27 and plane 21 is less, and required construction length is less, but pressure Loss increased even more.Or in other words：The surface of deflection piece is substantially provided in transverse plane, and the transverse plane is relative In at 45 ° to 90 ° angle arrangements of longitudinal axis, preferably into 60 ° to 90 ° angles, particularly preferably into 75 ° to 90 ° angles.It also will be understood that Deflection piece 27 is consistent with Fig. 1 as wall segment 3；However, comparing with the wall segment of Fig. 1, blending space 20 is divided into 4 Divide space.The cross section for being flowed through partly is reduced to the deflection piece two in 4 segment spaces.According to Fig. 3, these portions Each in point space is a fan（Shape）Area, when cross-sectional flow area is circle, the sector is with 90 ° of aperture Angle.As its alternative, when deflection piece is also designed to for the mixer case with square cross section, the portion Each divided in space can also have foursquare cross section.In this case, the bending of the deflection piece shown in replacing, four The deflection piece of side shape thus must be provided with adjacent with the unshowned inwall of tubular shell（Respectively）Edge.
Another embodiment of static mixer is shown in Fig. 4, wherein can be divided into fluid stream in the cross-direction Plural part stream.Included in blender tubular shell according to the plastic static mixer of Fig. 4 Mounting body（Or apparatus main body）1, wherein mounting body 1,101 has longitudinal axis 10, and the longitudinal axis 10 are led along installation is flowed into The direction arrangement of the fluid of body 1,101, so that the mounting body 1,101 can cross over blending space 20,120, wherein mixing is empty Between 20,120 in the plane 21,121 of longitudinal axis 10 have cross-sectional flow area 22,122, the cross-sectional flowing Area 22,122 corresponds essentially to the cross-sectional flow area of blender tubular shell, and wherein mounting body 1,101 includes wall Shape part 2,3,4,102,103,104, deflects into the side for deviateing longitudinal axis for separating and/or making the fluid stream by fluid stream Upwards.Cross-sectional area 23,123 can be produced by making wall segment 2,3,4,102,103,104 intersect with plane 21,121, and It is and the maximum of the cross-sectional area 23,123 reaches the 1/5 of the cross-sectional flow area 22,122 of blending space 20,120, excellent Selection of land be its 1/10, particularly preferably be its 1/20.Mounting body 1 includes multiple wall segments 2,3,4, each wall segment 2, 3rd, 4 all have the cross section of substantial rectangular, each described wall segment include first it is wide to while 5, second it is wide to while 6 and One longitudinal side and second longitudinal direction side 25,35.Each in wall segment 2,3,4 is arranged in mounting body 1, so that Longitudinal side 25,35 substantially longitudinally 10 direction extend and first it is wide to while 5 and second it is wide to while 6 relative to the longitudinal axis Line is extended transversely with.The mounting body includes the first wall segment 2 that blending space is divided into two parts, with the first wall-like Intersecting at least two wall segments, 3,4 adjacent first wall segment 2 of part 2.In the embodiment according to Fig. 4, the angle of intersection reaches 90 °, but the angle of intersection can adopt different value.According to Fig. 4, the first wall segment 2 by least one transition piece 11,12, 13rd, 111,112,113 are connected with the second wall segment 3 and the 3rd wall segment 4.As figure 3 illustrates, can will be described Transition piece is designed as fluid stream is deflected into from a subregion of cross-sectional flow area inclined in another subregion Turn part.
Adjacent mounting body 1,101 can be connected with each other by least one connector 14,15,114,115, this connection Part increases the bending rigidity of static mixer.Additionally, ensure that polymer melt can be installed from first by the connector Main body 1 is flowed to the first mounting body 101（With any other the other mounting body for being arranged in downstream）.If there is no these Connector, then from wall segment 3 or 4 to the transition of the wall segment 102 for being arranged on downstream clearly by unique public intersecting Surface is constituted, and the public intersection surface is made up of two squares in this case, and the foursquare length of side is equal to wall Thick 7.Whole polymer melts for being arranged on the mounting body in downstream must be by these restriction points, and this will lead in the tool Cause local pressure peak value.In addition, the dwell time of the length of polymer melt by cause wall segment when in use be located at tubulose There is such situation in some regions of housing adjacent, polymer melt can be made to change, and in some cases, cause material The deterioration of the physical property of material and inhomogeneities.It is particularly when foaming structure is produced using the melt containing foaming agent, this Dead band will be unfavorable for injection moulding process.
Similar to the mode shown in Fig. 4, these connectors are may be alternatively provided in the embodiment according to Fig. 1 or 2, however, its It is omitted to simplify the description of Fig. 1 and 2.The transition piece 27 of Fig. 3 can equally meet the function of connector.
According to Fig. 4, adjacent mounting body 1,101 is rotated into 180 ° of angles around longitudinal axis 10.Appoint according in previous embodiment The mounting body of one can be combined each other as required or be combined.Especially, other connector can also be provided with will not With mounting body combination with one another or the combination of embodiment, mixed effect is improved to form mixed structure.
According to of any one of previous embodiment, static mixer is made of plastics, even can be in injection moulding process by plastics It is middle to obtain even increasingly complex geometry.It is in particular for the static mixer including multiple mounting bodies, all to install Main body（1,101,201,301 ...）Each for all having in longitudinal size 24, and cross-sectional area 23,123 has wall thickness 7.The longitudinal size 24 reaches at least 40, preferably at least 50 with the ratio of the wall thickness 7, particularly preferably at least 75.For For the preferred application of the static mixer of small fluid volumes, wall thickness 7 is less than 3mm, preferably less than 2mm, particularly preferably be less than 1.5mm.The longitudinal size 24 of all mounting bodies 1,101 preferably between 5 to 300mm, preferentially exists between 5 to 500mm Between 50 to 100mm.
Through experiment, the longitudinal ruler with 60mm can be manufactured into foaming structure according to the static mixer of fourth embodiment The average wall thickness of very little and 0.42mm.Thus, flow path reaches 143 with the ratio of wall thickness:1.This blender is installed by 12 and is led Body is constituted.
Additionally, the longitudinal size with 100mm can be manufactured into foaming structure according to the static mixer of 3rd embodiment With the average wall thickness of 0.42mm.Thus, flow path reaches 238 with the ratio of wall thickness:1.The blender is by 24 mounting bodies Composition.

Claims (10)

1. a kind of static mixer, the static mixer include：
Tubular shell, the tubular shell have longitudinal axis and determine flow path for fluid；At least two mounting bodies, Link together during at least two mounting body is arranged on the tubular shell and in a coaxial relationship relative to each other, be used for Mixing flows through the fluid of the flow path of the tubular shell, and each at least two mounting body is with respect to which In another rotation, each described mounting body is the foamed plastic part manufactured by injection mo(u)lding, and described in each Mounting body has longitudinal size, width dimensions and a wall thickness, wherein the longitudinal size of each mounting body with it is described The ratio of width dimensions reaches at least 1；And wherein the longitudinal size of each mounting body is reached with the ratio of the wall thickness At least 10.
2. static mixer as claimed in claim 1, it is characterised in that at least one of described at least two mounting body With longitudinal axis, the longitudinal axis align along the direction of the longitudinal axis of the tubular shell, and described at least one installs , across the tubular shell to determine blending space, the blending space is perpendicular at least one mounting body for main body There is in the plane of the longitudinal axis cross-sectional flow area, at least one mounting body has at least one wall like portions Part, deflects into the direction for deviateing longitudinal direction for separating and/or making the fluid stream by fluid stream；And wherein by described Wall segment intersects generation cross-sectional area with the plane, and the maximum of the cross-sectional area reaches the horizontal stroke of the blending space The 1/5 of the flow area for cuing open.
3. static mixer as claimed in claim 2, it is characterised in that the blending space is divided into two by the wall segment Individual subregion.
4. static mixer as claimed in claim 2, it is characterised in that the wall segment includes bars, the strip First width of part forms shunting edge to side, and the bars include the second width to side, and second width is to side and deflection piece phase Neighbour, the deflection piece is for deflecting into the blending space by the fluid stream in the Part I region from the blending space In Part II region.
5. static mixer as claimed in claim 4, it is characterised in that from first it is wide to while, the second width to while and it is described The surface of the wall segment that the longitudinal side of wall segment is defined is substantially in described at least one institute for installing body State.
6. static mixer as claimed in claim 5, it is characterised in that the surface of the wall segment is arranged on transverse plane Interior, the transverse plane is relative to described at least one at 45 ° to 90 ° angles of the longitudinal axis for installing body.
7. static mixer as claimed in claim 5, it is characterised in that the surface of the wall segment is arranged on transverse plane Interior, the transverse plane installs the longitudinal axis of body into 60 ° to 90 ° angles relative to described at least one.
8. static mixer as claimed in claim 5, it is characterised in that the surface of the wall segment is arranged on transverse plane Interior, the transverse plane installs the longitudinal axis of body into 75 ° to 90 ° angles relative to described at least one.
9. static mixer as claimed in claim 1, it is characterised in which also includes multiple connectors, the connector exists It is longitudinally extending and at least two mounting body links together in the tubular shell.
10. a kind of method that the mounting body for static mixer is manufactured with injection moulding process, methods described comprise the following steps： In decanting point with the injection pressure less than 500 bars by the polymer melt injection channel comprising foaming agent；With it is described comprising send out The polymer melt of infusion fills the passage, and the polymer melt comprising foaming agent is at least partly risen in the passage Bubble, wherein the flow path of the polymer melt comprising foaming agent reaches at least 10 with the ratio of wall thickness, methods described is also wrapped Include the following steps：The polymer melt of at least part of foaming comprising foaming agent being cooled in the passage；Make the polymerization Thing melt solidifies to form the static mixer；Expand the cross section of the passage；Remove the mounting body.
CN201310742011.2A 2008-10-17 2009-10-19 Static mixer Active CN103861490B (en)

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TW201026479A (en) 2010-07-16
CA2680988A1 (en) 2010-04-17
BRPI0904183A2 (en) 2010-12-21
JP2010094999A (en) 2010-04-30
JP5889346B2 (en) 2016-03-22
KR20100043019A (en) 2010-04-27
IL201532A0 (en) 2010-06-16
EP2181827A2 (en) 2010-05-05
EP2181827A3 (en) 2017-11-29
AU2009227820A1 (en) 2010-05-06
CN103861490A (en) 2014-06-18
JP5623058B2 (en) 2014-11-12
EP2181827B1 (en) 2019-12-18
JP2014133416A (en) 2014-07-24
US8753006B2 (en) 2014-06-17
US20100097883A1 (en) 2010-04-22
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KR101729591B1 (en) 2017-04-24
RU2009138357A (en) 2011-04-27

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